Mixture of 1-Pentanol + Propanoic acid
Datasets
-
Azeotropic composition: mole fraction (6)
-
n0 - Refractive index (Na D-line) (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Azeotropic composition: mole fraction of 1-Pentanol (1)
[ref]
| Temperature, K - Liquid |
Azeotropic composition: mole fraction of 1-Pentanol (1) - Liquid |
| 397.25 |
0.4585 |
| 413.25 |
0.4390 |
Azeotropic composition: mole fraction of 1-Pentanol (1)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of 1-Pentanol (1) - Liquid |
| 53.30 |
0.4585 |
| 91.30 |
0.4390 |
Mole fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Gas |
Mole fraction of 1-Pentanol (1) - Gas |
| 0.0000 |
53.30 |
0.0000 |
| 0.0000 |
91.30 |
0.0000 |
| 0.0270 |
91.30 |
0.0180 |
| 0.0920 |
53.30 |
0.0720 |
| 0.1016 |
91.30 |
0.0705 |
| 0.1101 |
53.30 |
0.0902 |
| 0.1352 |
91.30 |
0.0996 |
| 0.1503 |
53.30 |
0.1174 |
| 0.1840 |
91.30 |
0.1409 |
| 0.1910 |
53.30 |
0.1499 |
| 0.2182 |
91.30 |
0.1864 |
| 0.2470 |
53.30 |
0.2001 |
| 0.2701 |
91.30 |
0.2392 |
| 0.2774 |
53.30 |
0.2349 |
| 0.3199 |
91.30 |
0.2985 |
| 0.3220 |
53.30 |
0.2940 |
| 0.3844 |
91.30 |
0.3721 |
| 0.3909 |
53.30 |
0.3692 |
| 0.4389 |
91.30 |
0.4391 |
| 0.4452 |
53.30 |
0.4391 |
| 0.4490 |
91.30 |
0.4502 |
| 0.4499 |
53.30 |
0.4412 |
| 0.4584 |
53.30 |
0.4582 |
| 0.4602 |
91.30 |
0.4657 |
| 0.4693 |
53.30 |
0.4698 |
| 0.4730 |
91.30 |
0.4796 |
| 0.4876 |
91.30 |
0.4969 |
| 0.4885 |
53.30 |
0.4912 |
| 0.5028 |
91.30 |
0.5142 |
| 0.5047 |
53.30 |
0.5173 |
| 0.5379 |
91.30 |
0.5604 |
| 0.5401 |
53.30 |
0.5638 |
| 0.5703 |
91.30 |
0.6040 |
| 0.5821 |
53.30 |
0.6059 |
| 0.6193 |
91.30 |
0.6651 |
| 0.6270 |
53.30 |
0.6640 |
| 0.6620 |
91.30 |
0.7030 |
| 0.6702 |
53.30 |
0.7202 |
| 0.7202 |
53.30 |
0.7690 |
| 0.7389 |
91.30 |
0.7996 |
| 0.7640 |
53.30 |
0.8180 |
| 0.7930 |
91.30 |
0.8450 |
| 0.8381 |
53.30 |
0.8703 |
| 0.8600 |
91.30 |
0.9111 |
| 0.9193 |
91.30 |
0.9514 |
| 0.9219 |
53.30 |
0.9297 |
| 0.9644 |
53.30 |
0.9821 |
| 0.9740 |
91.30 |
0.9903 |
| 1.0000 |
53.30 |
1.0000 |
| 1.0000 |
91.30 |
1.0000 |
Azeotropic composition: mole fraction of 1-Pentanol (1)
[ref]
| Temperature, K - Liquid |
Azeotropic composition: mole fraction of 1-Pentanol (1) - Liquid |
| 397.25 |
0.4585 |
| 413.25 |
0.4390 |
Azeotropic composition: mole fraction of 1-Pentanol (1)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of 1-Pentanol (1) - Liquid |
| 53.30 |
0.4585 |
| 91.30 |
0.4390 |
Mole fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Gas |
Mole fraction of 1-Pentanol (1) - Gas |
| 0.0000 |
53.30 |
0.0000 |
| 0.0000 |
91.30 |
0.0000 |
| 0.0270 |
91.30 |
0.0180 |
| 0.0920 |
53.30 |
0.0720 |
| 0.1016 |
91.30 |
0.0705 |
| 0.1101 |
53.30 |
0.0902 |
| 0.1352 |
91.30 |
0.0996 |
| 0.1503 |
53.30 |
0.1174 |
| 0.1840 |
91.30 |
0.1409 |
| 0.1910 |
53.30 |
0.1499 |
| 0.2182 |
91.30 |
0.1864 |
| 0.2470 |
53.30 |
0.2001 |
| 0.2701 |
91.30 |
0.2392 |
| 0.2774 |
53.30 |
0.2349 |
| 0.3199 |
91.30 |
0.2985 |
| 0.3220 |
53.30 |
0.2940 |
| 0.3844 |
91.30 |
0.3721 |
| 0.3909 |
53.30 |
0.3692 |
| 0.4389 |
91.30 |
0.4391 |
| 0.4452 |
53.30 |
0.4391 |
| 0.4490 |
91.30 |
0.4502 |
| 0.4499 |
53.30 |
0.4412 |
| 0.4584 |
53.30 |
0.4582 |
| 0.4602 |
91.30 |
0.4657 |
| 0.4693 |
53.30 |
0.4698 |
| 0.4730 |
91.30 |
0.4796 |
| 0.4876 |
91.30 |
0.4969 |
| 0.4885 |
53.30 |
0.4912 |
| 0.5028 |
91.30 |
0.5142 |
| 0.5047 |
53.30 |
0.5173 |
| 0.5379 |
91.30 |
0.5604 |
| 0.5401 |
53.30 |
0.5638 |
| 0.5703 |
91.30 |
0.6040 |
| 0.5821 |
53.30 |
0.6059 |
| 0.6193 |
91.30 |
0.6651 |
| 0.6270 |
53.30 |
0.6640 |
| 0.6620 |
91.30 |
0.7030 |
| 0.6702 |
53.30 |
0.7202 |
| 0.7202 |
53.30 |
0.7690 |
| 0.7389 |
91.30 |
0.7996 |
| 0.7640 |
53.30 |
0.8180 |
| 0.7930 |
91.30 |
0.8450 |
| 0.8381 |
53.30 |
0.8703 |
| 0.8600 |
91.30 |
0.9111 |
| 0.9193 |
91.30 |
0.9514 |
| 0.9219 |
53.30 |
0.9297 |
| 0.9644 |
53.30 |
0.9821 |
| 0.9740 |
91.30 |
0.9903 |
| 1.0000 |
53.30 |
1.0000 |
| 1.0000 |
91.30 |
1.0000 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Temperature, K = 293.15 (Liquid)
| Mole fraction of 1-Pentanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.381 |
| 0.0985 |
1.3838 |
| 0.1745 |
1.3861 |
| 0.2541 |
1.3884 |
| 0.3256 |
1.3904 |
| 0.3974 |
1.3925 |
| 0.4321 |
1.3935 |
| 0.5000 |
1.3955 |
| 0.5732 |
1.3976 |
| 0.6528 |
1.3999 |
| 0.7243 |
1.402 |
| 0.8001 |
1.4042 |
| 0.8759 |
1.4064 |
| 0.9324 |
1.4079 |
| 1.0000 |
1.41 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Temperature, K = 293.15 (Liquid)
| Mole fraction of 1-Pentanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.381 |
| 0.0985 |
1.3838 |
| 0.1745 |
1.3861 |
| 0.2541 |
1.3884 |
| 0.3256 |
1.3904 |
| 0.3974 |
1.3925 |
| 0.4321 |
1.3935 |
| 0.5000 |
1.3955 |
| 0.5732 |
1.3976 |
| 0.6528 |
1.3999 |
| 0.7243 |
1.402 |
| 0.8001 |
1.4042 |
| 0.8759 |
1.4064 |
| 0.9324 |
1.4079 |
| 1.0000 |
1.41 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
53.30 |
394.55 |
| 0.0000 |
91.30 |
410.55 |
| 0.0270 |
91.30 |
410.85 |
| 0.0920 |
53.30 |
395.45 |
| 0.1016 |
91.30 |
411.65 |
| 0.1101 |
53.30 |
395.60 |
| 0.1352 |
91.30 |
411.95 |
| 0.1503 |
53.30 |
395.85 |
| 0.1840 |
91.30 |
412.15 |
| 0.1910 |
53.30 |
396.25 |
| 0.2182 |
91.30 |
412.40 |
| 0.2470 |
53.30 |
396.65 |
| 0.2701 |
91.30 |
412.65 |
| 0.2774 |
53.30 |
396.85 |
| 0.3199 |
91.30 |
412.95 |
| 0.3220 |
53.30 |
397.00 |
| 0.3844 |
91.30 |
413.15 |
| 0.3909 |
53.30 |
397.20 |
| 0.4389 |
91.30 |
413.25 |
| 0.4452 |
53.30 |
397.25 |
| 0.4490 |
91.30 |
413.25 |
| 0.4499 |
53.30 |
397.25 |
| 0.4584 |
53.30 |
397.25 |
| 0.4602 |
91.30 |
413.25 |
| 0.4693 |
53.30 |
397.20 |
| 0.4730 |
91.30 |
413.20 |
| 0.4876 |
91.30 |
413.15 |
| 0.4885 |
53.30 |
397.20 |
| 0.5028 |
91.30 |
413.05 |
| 0.5047 |
53.30 |
397.15 |
| 0.5379 |
91.30 |
412.90 |
| 0.5401 |
53.30 |
397.05 |
| 0.5703 |
91.30 |
412.70 |
| 0.5821 |
53.30 |
396.95 |
| 0.6193 |
91.30 |
412.45 |
| 0.6270 |
53.30 |
396.75 |
| 0.6620 |
91.30 |
412.15 |
| 0.6702 |
53.30 |
396.50 |
| 0.7202 |
53.30 |
396.15 |
| 0.7389 |
91.30 |
411.35 |
| 0.7640 |
53.30 |
395.75 |
| 0.7930 |
91.30 |
410.65 |
| 0.8381 |
53.30 |
395.25 |
| 0.8600 |
91.30 |
409.85 |
| 0.9193 |
91.30 |
409.40 |
| 0.9219 |
53.30 |
394.35 |
| 0.9644 |
53.30 |
393.50 |
| 0.9740 |
91.30 |
408.55 |
| 1.0000 |
53.30 |
393.15 |
| 1.0000 |
91.30 |
408.05 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
53.30 |
394.55 |
| 0.0000 |
91.30 |
410.55 |
| 0.0270 |
91.30 |
410.85 |
| 0.0920 |
53.30 |
395.45 |
| 0.1016 |
91.30 |
411.65 |
| 0.1101 |
53.30 |
395.60 |
| 0.1352 |
91.30 |
411.95 |
| 0.1503 |
53.30 |
395.85 |
| 0.1840 |
91.30 |
412.15 |
| 0.1910 |
53.30 |
396.25 |
| 0.2182 |
91.30 |
412.40 |
| 0.2470 |
53.30 |
396.65 |
| 0.2701 |
91.30 |
412.65 |
| 0.2774 |
53.30 |
396.85 |
| 0.3199 |
91.30 |
412.95 |
| 0.3220 |
53.30 |
397.00 |
| 0.3844 |
91.30 |
413.15 |
| 0.3909 |
53.30 |
397.20 |
| 0.4389 |
91.30 |
413.25 |
| 0.4452 |
53.30 |
397.25 |
| 0.4490 |
91.30 |
413.25 |
| 0.4499 |
53.30 |
397.25 |
| 0.4584 |
53.30 |
397.25 |
| 0.4602 |
91.30 |
413.25 |
| 0.4693 |
53.30 |
397.20 |
| 0.4730 |
91.30 |
413.20 |
| 0.4876 |
91.30 |
413.15 |
| 0.4885 |
53.30 |
397.20 |
| 0.5028 |
91.30 |
413.05 |
| 0.5047 |
53.30 |
397.15 |
| 0.5379 |
91.30 |
412.90 |
| 0.5401 |
53.30 |
397.05 |
| 0.5703 |
91.30 |
412.70 |
| 0.5821 |
53.30 |
396.95 |
| 0.6193 |
91.30 |
412.45 |
| 0.6270 |
53.30 |
396.75 |
| 0.6620 |
91.30 |
412.15 |
| 0.6702 |
53.30 |
396.50 |
| 0.7202 |
53.30 |
396.15 |
| 0.7389 |
91.30 |
411.35 |
| 0.7640 |
53.30 |
395.75 |
| 0.7930 |
91.30 |
410.65 |
| 0.8381 |
53.30 |
395.25 |
| 0.8600 |
91.30 |
409.85 |
| 0.9193 |
91.30 |
409.40 |
| 0.9219 |
53.30 |
394.35 |
| 0.9644 |
53.30 |
393.50 |
| 0.9740 |
91.30 |
408.55 |
| 1.0000 |
53.30 |
393.15 |
| 1.0000 |
91.30 |
408.05 |
Sources